CN104817714A - Adamantane structure-containing polyarylether anion-exchange membrane and preparation method thereof - Google Patents
Adamantane structure-containing polyarylether anion-exchange membrane and preparation method thereof Download PDFInfo
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- CN104817714A CN104817714A CN201510131463.6A CN201510131463A CN104817714A CN 104817714 A CN104817714 A CN 104817714A CN 201510131463 A CN201510131463 A CN 201510131463A CN 104817714 A CN104817714 A CN 104817714A
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- adamantane structure
- polyarylether
- containing adamantane
- structure polyarylether
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- ORILYTVJVMAKLC-UHFFFAOYSA-N adamantane Chemical group C1C(C2)CC3CC1CC2C3 ORILYTVJVMAKLC-UHFFFAOYSA-N 0.000 title claims abstract description 90
- 229920000090 poly(aryl ether) Polymers 0.000 title claims abstract description 75
- 239000003011 anion exchange membrane Substances 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- 239000012528 membrane Substances 0.000 claims abstract description 32
- 238000005576 amination reaction Methods 0.000 claims abstract description 18
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 14
- 230000004048 modification Effects 0.000 claims abstract description 10
- 238000012986 modification Methods 0.000 claims abstract description 10
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims abstract description 3
- 239000002904 solvent Substances 0.000 claims description 22
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 15
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 claims description 12
- 229920000642 polymer Polymers 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 claims description 10
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 10
- 238000005266 casting Methods 0.000 claims description 10
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims description 9
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical group ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 8
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 6
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 5
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 5
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 4
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 4
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 claims description 4
- VNDYJBBGRKZCSX-UHFFFAOYSA-L zinc bromide Chemical compound Br[Zn]Br VNDYJBBGRKZCSX-UHFFFAOYSA-L 0.000 claims description 4
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 4
- HRQGCQVOJVTVLU-UHFFFAOYSA-N bis(chloromethyl) ether Chemical compound ClCOCCl HRQGCQVOJVTVLU-UHFFFAOYSA-N 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 claims description 3
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 3
- NEFNOUUWYACOKP-UHFFFAOYSA-N 1-(chloromethoxy)butane Chemical compound CCCCOCCl NEFNOUUWYACOKP-UHFFFAOYSA-N 0.000 claims description 2
- YUMNZEWYPUBSQA-UHFFFAOYSA-N 1-(chloromethoxy)octane Chemical compound CCCCCCCCOCCl YUMNZEWYPUBSQA-UHFFFAOYSA-N 0.000 claims description 2
- MCTWTZJPVLRJOU-UHFFFAOYSA-N 1-methyl-1H-imidazole Chemical compound CN1C=CN=C1 MCTWTZJPVLRJOU-UHFFFAOYSA-N 0.000 claims description 2
- XJUZRXYOEPSWMB-UHFFFAOYSA-N Chloromethyl methyl ether Chemical compound COCCl XJUZRXYOEPSWMB-UHFFFAOYSA-N 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 2
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 claims description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- JAMFGQBENKSWOF-UHFFFAOYSA-N bromo(methoxy)methane Chemical compound COCBr JAMFGQBENKSWOF-UHFFFAOYSA-N 0.000 claims description 2
- 229940061627 chloromethyl methyl ether Drugs 0.000 claims description 2
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 239000012046 mixed solvent Substances 0.000 claims description 2
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims description 2
- 239000000376 reactant Substances 0.000 claims description 2
- IMFACGCPASFAPR-UHFFFAOYSA-N tributylamine Chemical compound CCCCN(CCCC)CCCC IMFACGCPASFAPR-UHFFFAOYSA-N 0.000 claims description 2
- ITMCEJHCFYSIIV-UHFFFAOYSA-N triflic acid Chemical compound OS(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-N 0.000 claims description 2
- YFTHZRPMJXBUME-UHFFFAOYSA-N tripropylamine Chemical compound CCCN(CCC)CCC YFTHZRPMJXBUME-UHFFFAOYSA-N 0.000 claims description 2
- 229940102001 zinc bromide Drugs 0.000 claims description 2
- 235000005074 zinc chloride Nutrition 0.000 claims description 2
- 239000011592 zinc chloride Substances 0.000 claims description 2
- 210000004379 membrane Anatomy 0.000 claims 11
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims 4
- 210000002469 basement membrane Anatomy 0.000 claims 4
- 238000001556 precipitation Methods 0.000 claims 4
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 claims 2
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical compound O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 claims 2
- 238000007654 immersion Methods 0.000 claims 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims 2
- NKJOXAZJBOMXID-UHFFFAOYSA-N 1,1'-Oxybisoctane Chemical compound CCCCCCCCOCCCCCCCC NKJOXAZJBOMXID-UHFFFAOYSA-N 0.000 claims 1
- DURPTKYDGMDSBL-UHFFFAOYSA-N 1-butoxybutane Chemical compound CCCCOCCCC DURPTKYDGMDSBL-UHFFFAOYSA-N 0.000 claims 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims 1
- 239000004411 aluminium Substances 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- PQLAYKMGZDUDLQ-UHFFFAOYSA-K aluminium bromide Chemical compound Br[Al](Br)Br PQLAYKMGZDUDLQ-UHFFFAOYSA-K 0.000 claims 1
- 229940055858 aluminum chloride anhydrous Drugs 0.000 claims 1
- 230000008020 evaporation Effects 0.000 claims 1
- 229940032296 ferric chloride Drugs 0.000 claims 1
- 229940015043 glyoxal Drugs 0.000 claims 1
- GYCHYNMREWYSKH-UHFFFAOYSA-L iron(ii) bromide Chemical compound [Fe+2].[Br-].[Br-] GYCHYNMREWYSKH-UHFFFAOYSA-L 0.000 claims 1
- 230000000873 masking effect Effects 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 239000003921 oil Substances 0.000 claims 1
- 239000000843 powder Substances 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 229960004418 trolamine Drugs 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 229910052725 zinc Inorganic materials 0.000 claims 1
- 239000011701 zinc Substances 0.000 claims 1
- 229910052720 vanadium Inorganic materials 0.000 abstract description 9
- 239000000126 substance Substances 0.000 abstract description 6
- 150000003384 small molecules Chemical class 0.000 abstract description 5
- 150000002500 ions Chemical class 0.000 abstract description 4
- 238000005349 anion exchange Methods 0.000 abstract description 3
- 238000004146 energy storage Methods 0.000 abstract description 3
- 239000000446 fuel Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 12
- 239000002585 base Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 229910002804 graphite Inorganic materials 0.000 description 4
- 239000010439 graphite Substances 0.000 description 4
- 229920000412 polyarylene Polymers 0.000 description 4
- 229920006260 polyaryletherketone Polymers 0.000 description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 229920000557 Nafion® Polymers 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 238000005342 ion exchange Methods 0.000 description 3
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 2
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 125000004218 chloromethyl group Chemical group [H]C([H])(Cl)* 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 238000000909 electrodialysis Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- -1 halomethyl alkyl ether Chemical class 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 229910001456 vanadium ion Inorganic materials 0.000 description 2
- RTSBCGFVAMIDBC-UHFFFAOYSA-N 1-(bromomethoxy)butane Chemical compound CCCCOCBr RTSBCGFVAMIDBC-UHFFFAOYSA-N 0.000 description 1
- PMGWYOXUKDCMNK-UHFFFAOYSA-N 1-(bromomethoxy)octane Chemical compound CCCCCCCCOCBr PMGWYOXUKDCMNK-UHFFFAOYSA-N 0.000 description 1
- LXBGSDVWAMZHDD-UHFFFAOYSA-N 2-methyl-1h-imidazole Chemical compound CC1=NC=CN1 LXBGSDVWAMZHDD-UHFFFAOYSA-N 0.000 description 1
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical group COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 1
- BDAGIHXWWSANSR-UHFFFAOYSA-N Formic acid Chemical compound OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 1
- 229920000491 Polyphenylsulfone Polymers 0.000 description 1
- YSVZGWAJIHWNQK-UHFFFAOYSA-N [3-(hydroxymethyl)-2-bicyclo[2.2.1]heptanyl]methanol Chemical compound C1CC2C(CO)C(CO)C1C2 YSVZGWAJIHWNQK-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- CYYWAXVARNZFBI-UHFFFAOYSA-N bromomethoxyethane Chemical compound CCOCBr CYYWAXVARNZFBI-UHFFFAOYSA-N 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- FCYRSDMGOLYDHL-UHFFFAOYSA-N chloromethoxyethane Chemical compound CCOCCl FCYRSDMGOLYDHL-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 125000001165 hydrophobic group Chemical group 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000002608 ionic liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- PUGUQINMNYINPK-UHFFFAOYSA-N tert-butyl 4-(2-chloroacetyl)piperazine-1-carboxylate Chemical compound CC(C)(C)OC(=O)N1CCN(C(=O)CCl)CC1 PUGUQINMNYINPK-UHFFFAOYSA-N 0.000 description 1
- FEONEKOZSGPOFN-UHFFFAOYSA-K tribromoiron Chemical compound Br[Fe](Br)Br FEONEKOZSGPOFN-UHFFFAOYSA-K 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
含金刚烷结构聚芳醚阴离子交换膜及其制备方法。涉及一种化工膜分离材料及其制备方法,该方法将含金刚烷结构聚芳醚进行卤甲基化改性,得到卤甲基化程度为10~200%的卤甲基化含金刚烷结构聚芳醚。将卤甲基化含金刚烷结构聚芳醚与含氮有机小分子进行胺化反应,引入阴离子交换基团,制备含金刚烷结构聚芳醚阴离子交换膜,所制备的含金刚烷结构聚芳醚阴离子交换膜具有高的离子传导性,优良的渗透选择性和化学稳定性,可作为全钒液流储能电池和碱性燃料电池的隔膜,具有很好的应用前景。Polyarylether anion exchange membrane containing adamantane structure and its preparation method. It relates to a chemical membrane separation material and a preparation method thereof. In the method, a polyarylether containing an adamantane structure is subjected to halomethylation modification to obtain a halomethylation containing an adamantane structure with a halomethylation degree of 10 to 200%. Polyarylether. The amination reaction of halomethylated polyarylether containing adamantane structure and nitrogen-containing organic small molecules is carried out to introduce anion exchange groups to prepare polyarylether anion exchange membrane containing adamantane structure. The prepared polyarylether containing adamantane structure Ether anion exchange membranes have high ion conductivity, excellent permeation selectivity and chemical stability, and can be used as diaphragms for all-vanadium flow energy storage batteries and alkaline fuel cells, with good application prospects.
Description
技术领域 technical field
本发明涉及一种化工膜分离材料及其制备方法,特别是涉及一种含金刚烷结构聚芳醚阴离子交换膜及其制备方法。 The invention relates to a chemical membrane separation material and a preparation method thereof, in particular to an adamantane-containing polyarylether anion exchange membrane and a preparation method thereof.
背景技术 Background technique
阴离子交换膜可用于电渗析浓缩海水制盐、电渗析咸水淡化、工业废水处理、电解、扩散渗析酸(碱)回收、燃料电池、液流储能电池及其他需要阴离子交换膜的新技术应用领域。在全钒液流储能电池中,要求膜具有高离子传导性,优良的渗透选择性和化学稳定性。商业化芳基聚合物如聚砜、聚苯砜等膜材料在高离子交换容量时,膜的含水率大,溶胀严重,尺寸稳定性和机械强度下降,膜的稳定性差。将刚性扭曲结构、疏水性基团引入聚合物中控制膜的含水率,降低膜溶胀。金刚烷是刚性笼状的饱和碳氢化合物,具有高热稳定性、强疏水性,将金刚烷引入聚合物获得刚性扭曲结构单元,增加分子链的刚性,提高聚合物热稳定性,提升聚合物链疏水性,调节膜的亲水-疏水平衡,提高膜稳定性。 Anion exchange membranes can be used for electrodialysis concentrated seawater salt production, electrodialysis salt water desalination, industrial wastewater treatment, electrolysis, diffusion dialysis acid (alkali) recovery, fuel cells, liquid flow energy storage batteries and other new technology applications that require anion exchange membranes field. In all-vanadium redox flow energy storage batteries, the membrane is required to have high ion conductivity, excellent permeation selectivity and chemical stability. When commercial aryl polymers such as polysulfone and polyphenylsulfone have a high ion exchange capacity, the water content of the membrane is high, the swelling is severe, the dimensional stability and mechanical strength are reduced, and the stability of the membrane is poor. The rigid twisted structure and hydrophobic groups are introduced into the polymer to control the water content of the membrane and reduce the swelling of the membrane. Adamantane is a rigid cage-like saturated hydrocarbon with high thermal stability and strong hydrophobicity. Introducing adamantane into a polymer to obtain a rigid twisted structural unit increases the rigidity of the molecular chain, improves the thermal stability of the polymer, and enhances the polymer chain. Hydrophobicity, adjust the hydrophilic-hydrophobic balance of the membrane, and improve the stability of the membrane.
发明内容 Contents of the invention
本发明的目的在于提供一种含金刚烷结构聚芳醚阴离子交换膜及其制备方法,该方法以含金刚烷结构聚芳醚为原料,经卤甲基化、胺化,将阴离子交换基团引入含金刚烷结构聚芳醚中,制备含金刚烷结构聚芳醚阴离子交换膜。制备的含金刚烷结构聚芳醚阴离子交换膜具有高的离子传导性、优良的选择透过性和化学稳定性。 The object of the present invention is to provide a polyarylether anion exchange membrane containing an adamantane structure and a preparation method thereof. The method uses a polyarylether containing an adamantane structure as a raw material, and through halomethylation and amination, the anion exchange group The polyarylether containing adamantane structure is introduced into the polyarylether containing adamantane structure to prepare the polyarylether anion exchange membrane containing adamantane structure. The prepared polyarylether anion exchange membrane containing adamantane structure has high ion conductivity, excellent selective permeability and chemical stability.
本发明的目的是通过以下技术方案实现的: The purpose of the present invention is achieved through the following technical solutions:
含金刚烷结构聚芳醚阴离子交换膜,由含金刚烷结构聚芳醚经卤甲基化、胺化处理步骤制备得到,含金刚烷结构聚芳醚的聚合物分子链含有如下结构: The polyarylether anion exchange membrane containing adamantane structure is prepared by the steps of halomethylation and amination of polyarylether containing adamantane structure. The polymer molecular chain of polyarylether containing adamantane structure contains the following structure:
含金刚烷结构聚芳醚的阴离子交换膜的制备方法,包括以下步骤: A method for preparing an anion-exchange membrane containing polyarylether with adamantane structure, comprising the following steps:
含金刚烷结构聚芳醚溶解于溶剂中,加入卤甲基烷基醚和催化剂,一定温度下搅拌反应。反应结束后,将反应物倒入沉淀剂中,分离、洗涤、干燥,得到卤甲基化含金刚烷结构聚芳醚。卤甲基化含金刚烷结构聚芳醚的结构简式如下: The polyarylether containing adamantane structure is dissolved in the solvent, and the halomethyl alkyl ether and catalyst are added, and the reaction is stirred at a certain temperature. After the reaction, the reactant is poured into a precipitant, separated, washed and dried to obtain the halomethylated adamantane-containing polyarylether. The structural formula of halomethylated polyarylether containing adamantane structure is as follows:
将卤甲基化含金刚烷结构聚芳醚溶解于溶剂中配制成铸膜液,铸膜,将溶剂完全蒸发或部分蒸发后浸入沉淀剂中,制得卤甲基化含金刚烷结构聚芳醚基膜。制备卤甲基化含金刚烷结构聚芳醚基膜的烘膜温度为10 oC -150 oC,时间0-48小时;所用沉淀剂为水、甲醇、乙醇、丙醇、异丙醇、丙酮、乙醚、丁酮、乙酸乙酯中的一种或两种以上的混合溶剂。将卤甲基化含金刚烷结构聚芳醚基膜浸泡于含氮有机小分子溶液中进行胺化处理,得到含金刚烷结构聚芳醚阴离子交换膜。胺化处理温度为0oC-90oC,时间为0-96小时。 Dissolving halomethylated polyarylene ether containing adamantane structure in a solvent to prepare a casting solution, casting a film, immersing the solvent in a precipitating agent after completely evaporating or partially evaporating, to obtain a halomethylated polyarylene containing adamantane structure ether-based film. The baking temperature of the halomethylated polyarylether base film containing adamantane structure is 10 o C -150 o C, and the time is 0-48 hours; the precipitant used is water, methanol, ethanol, propanol, isopropanol, acetone , ether, methyl ethyl ketone, ethyl acetate or a mixed solvent of two or more. Soaking the halomethylated polyarylether base membrane containing the adamantane structure in a nitrogen-containing organic small molecule solution for amination treatment to obtain the polyarylether anion exchange membrane containing the adamantane structure. The amination treatment temperature is 0 o C-90 o C, and the time is 0-96 hours.
含金刚烷结构聚芳醚阴离子交换膜也可以通过先胺化后制膜的方法实现:将卤甲基化含金刚烷结构聚芳醚溶解于溶剂中配制成溶液,加入含氮有机小分子进行胺化反应,反应温度为0~90 oC,反应时间为0~96小时;胺化反应后的溶液铸膜,将溶剂完全蒸发或部分蒸发后浸入沉淀剂中,得到含金刚烷结构聚芳醚阴离子交换膜,烘膜温度为10~150oC,烘膜时间为0~48小时。 The polyarylether anion exchange membrane containing adamantane structure can also be realized by the method of amination first and then membrane formation: the halomethylated polyarylether containing adamantane structure is dissolved in a solvent to prepare a solution, and nitrogen-containing organic small molecules are added to carry out Amination reaction, the reaction temperature is 0-90 o C, and the reaction time is 0-96 hours; the solution after the amination reaction is cast into a film, and the solvent is completely evaporated or partially evaporated and then immersed in a precipitant to obtain a polyarylene containing adamantane structure. For ether anion exchange membrane, the drying temperature is 10~150 o C, and the drying time is 0~48 hours.
本发明所述含金刚烷结构聚芳醚的卤甲基化改性所使用的卤甲基烷基醚可以为氯甲基甲醚、氯甲基乙醚、、氯甲基丁醚、氯甲基辛醚、溴甲基甲醚、溴甲基乙醚、溴甲基丁醚、溴甲基辛醚。含金刚烷结构聚芳醚的卤甲基化改性所用的催化剂可以为无水氯化锌、无水氯化铁、无水氯化铝、无水溴化锌、无水溴化铁、无水溴化铝、金属锌粉、金属铁粉、金属铝粉、无水四氯化锡、浓硫酸、浓盐酸、磷酸、氯铝酸离子液体或三氟甲基磺酸中的一种或上述催化剂的混合物。 The halomethyl alkyl ether used in the halomethylation modification of polyarylether containing adamantane structure in the present invention can be chloromethyl methyl ether, chloromethyl ethyl ether, chloromethyl butyl ether, chloromethyl Octyl ether, bromomethyl methyl ether, bromomethyl ethyl ether, bromomethyl butyl ether, bromomethyl octyl ether. The catalyst used for the halomethylation modification of polyarylether containing adamantane structure can be anhydrous zinc chloride, anhydrous ferric chloride, anhydrous aluminum chloride, anhydrous zinc bromide, anhydrous ferric bromide, anhydrous Aluminum bromide in water, metal zinc powder, metal iron powder, metal aluminum powder, anhydrous tin tetrachloride, concentrated sulfuric acid, concentrated hydrochloric acid, phosphoric acid, chloroaluminate ionic liquid or trifluoromethanesulfonic acid or one or the above mixture of catalysts.
本发明所述含金刚烷结构聚芳醚的卤甲基化改性所用溶剂可以为氯仿、二氯甲烷、二氯乙烷、四氯乙烷、硝基苯、氯苯或浓硫酸。 The solvent used for the halomethylation modification of polyarylether containing adamantane structure in the present invention can be chloroform, dichloromethane, dichloroethane, tetrachloroethane, nitrobenzene, chlorobenzene or concentrated sulfuric acid.
本发明所述含金刚烷结构聚芳醚的卤甲基化改性的反应温度为-10 oC -120oC,反应时间为1-72小时。 The reaction temperature of the halomethylation modification of polyarylether containing adamantane structure in the present invention is -10 o C -120 o C, and the reaction time is 1-72 hours.
本发明所述卤甲基化含金刚烷结构聚芳醚基膜的制备可以采用氯仿、二氯甲烷、二氯乙烷、二甲基亚砜、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、N-甲基-2-吡咯烷酮或上述溶剂的混合溶液为配制铸膜液的溶剂。 The preparation of the halomethylated polyarylether-based film containing adamantane structure in the present invention can adopt chloroform, dichloromethane, dichloroethane, dimethylsulfoxide, N,N -dimethylformamide, N, N -dimethylacetamide, N -methyl-2-pyrrolidone or a mixed solution of the above solvents are solvents for preparing the casting solution.
本发明所述制备卤甲基化含金刚烷结构聚芳醚的铸膜时的烘膜温度可以为10-150oC,优选30-120oC,时间0-48小时,沉淀剂可以采用甲醇、乙醇、水或上述溶剂中的一种或两种溶剂的混合溶液。 The drying film temperature when preparing the cast film of halomethylated polyarylether containing adamantane structure according to the present invention can be 10-150 o C, preferably 30-120 o C, and the time is 0-48 hours, and the precipitating agent can be methanol , ethanol, water or one or a mixed solution of two solvents in the above solvents.
本发明所述的卤甲基化含金刚烷结构聚芳醚的胺化处理所采用的试剂可以为含氮有机小分子,所采用的含氮有机小分子可以是三甲胺、三乙胺、三乙醇胺、三正丙胺、三正丁胺、吡啶、1-甲基咪唑、2-甲基咪唑中的一种或两种以上的混合物。 The reagents used in the amination treatment of halomethylated adamantane-containing polyarylethers described in the present invention can be nitrogen-containing organic small molecules, and the nitrogen-containing organic small molecules used can be trimethylamine, triethylamine, trimethylamine, triethylamine, or trimethylamine. One or a mixture of two or more of ethanolamine, tri-n-propylamine, tri-n-butylamine, pyridine, 1-methylimidazole, and 2-methylimidazole.
本发明所述卤甲基化含金刚烷结构聚芳醚的胺化处理温度可以为0oC-90oC,时间为0-96小时。含金刚烷结构聚芳醚阴离子交换膜的结构简式如下: The amination treatment temperature of the halomethylated polyarylether containing adamantane structure in the present invention can be 0 ° C-90 ° C, and the time is 0-96 hours. The structure of polyarylether anion exchange membrane containing adamantane structure is as follows:
本发明的优点与效果是: Advantage and effect of the present invention are:
本发明提出以含金刚烷结构聚芳醚为原料,经卤甲基化、胺化,将阴离子交换基团引入含金刚烷结构聚芳醚中,制备含金刚烷结构聚芳醚阴离子交换膜。制备的含金刚烷结构聚芳醚阴离子交换膜具有高的离子传导性、优良的选择透过性和化学稳定性,在液流电池和燃料电池等需要高性能阴离子交换膜的新技术领域具有广阔的应用前景。 The invention proposes to use polyarylether containing adamantane structure as raw material, and through halomethylation and amination, anion exchange groups are introduced into polyarylether containing adamantane structure to prepare polyarylether anion exchange membrane containing polyarylether with adamantane structure. The prepared polyarylether anion exchange membrane containing adamantane structure has high ion conductivity, excellent selective permeability and chemical stability, and has broad application in new technology fields requiring high-performance anion exchange membranes such as flow batteries and fuel cells. application prospects.
具体实施方式 Detailed ways
下面结合实施例对本发明进行详细说明。 The present invention will be described in detail below in conjunction with examples.
实施例列出了新型阴离子交换膜的制备工艺及性能,这些实例仅仅是为了对本发明进行说明,并不是限定本发明保护范围。 The examples list the preparation process and performance of the novel anion exchange membrane, these examples are only for illustrating the present invention, and are not intended to limit the protection scope of the present invention.
实施例1 Example 1
将5g含金刚烷结构聚芳醚酮溶解于50mL四氯乙烷中,升温至35oC,加入1mL四氯化锡,然后再加入5mL氯甲基乙醚,反应8小时后,将反应溶液倒入乙醇中,析出的聚合物用大量乙醇清洗,然后在真空烘箱中70oC干燥,得到氯甲基含量为2.3 mmol/g的氯甲基化含金刚烷结构聚芳醚。将干燥的氯甲基化含金刚烷结构聚芳醚溶于N-甲基吡咯烷酮中,配制成聚合物质量百分含量为10%的铸膜液。过滤后,将铸膜液倒在洁净的水平玻璃板上,刮制成膜,在60oC,挥发溶剂,得到厚度为50微米的基膜,然后浸泡于水中进一步除去溶剂。将基膜放于33%的三甲胺水溶液中,50oC下胺化72小时,然后将膜转移到5%稀盐酸中,浸泡2小时,再用去离子水清洗得到阴离子交换膜。该阴离子交换膜的离子交换容量为2.0 mmol/g。 Dissolve 5g of polyaryletherketone containing adamantane structure in 50mL of tetrachloroethane, heat up to 35 o C, add 1mL of tin tetrachloride, and then add 5mL of chloromethyl ether, react for 8 hours, pour the reaction solution into ethanol, the precipitated polymer was washed with a large amount of ethanol, and then dried in a vacuum oven at 70 o C to obtain a chloromethylated adamantane-containing polyarylether with a chloromethyl content of 2.3 mmol/g. The dried chloromethylated polyarylether containing adamantane structure is dissolved in N -methylpyrrolidone to prepare a casting solution with a polymer mass percentage of 10%. After filtering, pour the casting solution on a clean horizontal glass plate, scrape it into a film, and volatilize the solvent at 60 o C to obtain a base film with a thickness of 50 microns, and then soak it in water to further remove the solvent. The base membrane was placed in 33% trimethylamine aqueous solution, aminated at 50 o C for 72 hours, then transferred to 5% dilute hydrochloric acid, soaked for 2 hours, and then washed with deionized water to obtain an anion exchange membrane. The ion exchange capacity of this anion exchange membrane was 2.0 mmol/g.
实施例2 Example 2
将5g含金刚烷结构聚芳醚酮溶解于50mL四氯乙烷中,升温至50oC,加入2mL无水四氯化锡,然后再加入5mL氯甲基乙醚,反应10小时后,将反应溶液倒入乙醇中,析出的聚合物用大量乙醇清洗,然后在真空烘箱中70oC干燥,得到氯甲基含量为2.1 mmol/g的氯甲基化含金刚烷结构聚芳醚。将干燥的氯甲基化含金刚烷结构聚芳醚溶于N-甲基吡咯烷酮中,配制成聚合物质量百分含量为10%的铸膜液。过滤后,将铸膜液在洁净的水平玻璃板上,刮制成膜,在60oC,挥发溶剂,得到厚度为50微米的基膜,然后浸泡于水中进一步除去溶剂。将基膜放于33%的三甲胺水溶液中,50oC下胺化72小时,然后将膜转移到5%稀盐酸中,浸泡2小时,再用去离子水清洗得到含金刚烷结构聚芳醚阴离子交换膜。该阴离子交换膜的离子交换容量为1.9 mmol/g。 Dissolve 5g of polyaryletherketone containing adamantane structure in 50mL of tetrachloroethane, heat up to 50 o C, add 2mL of anhydrous tin tetrachloride, and then add 5mL of chloromethyl ether, and react for 10 hours. The solution was poured into ethanol, and the precipitated polymer was washed with a large amount of ethanol, and then dried in a vacuum oven at 70 o C to obtain a chloromethylated adamantane-containing polyarylether with a chloromethyl content of 2.1 mmol/g. The dried chloromethylated polyarylether containing adamantane structure is dissolved in N -methylpyrrolidone to prepare a casting solution with a polymer mass percentage of 10%. After filtering, scrape the casting solution on a clean horizontal glass plate to form a film, evaporate the solvent at 60 o C to obtain a base film with a thickness of 50 microns, and then soak it in water to further remove the solvent. Put the base film in 33% trimethylamine aqueous solution, and aminate it at 50 o C for 72 hours, then transfer the film to 5% dilute hydrochloric acid, soak it for 2 hours, and then wash it with deionized water to obtain polyarylene containing adamantane structure. ether anion exchange membrane. The ion exchange capacity of this anion exchange membrane was 1.9 mmol/g.
实施例3 Example 3
将实施例1中的含金刚烷结构聚芳醚酮阴离子交换膜组装全钒液流电池,石墨毡为电极,石墨板为双极板,膜有效面积为5cm2,电流密度为100 mA/cm2,电解液中钒离子浓度为1.5mol/L,H2SO4浓度为3 mol/L。组装的钒液流电池电流效率为99%,电压效率为83%,能量效率为82%。 An all-vanadium redox flow battery was assembled with the adamantane-containing polyaryletherketone anion exchange membrane in Example 1. The graphite felt was used as an electrode, and the graphite plate was used as a bipolar plate. The effective area of the membrane was 5 cm 2 , and the current density was 100 mA/cm 2. The concentration of vanadium ions in the electrolyte is 1.5 mol/L, and the concentration of H 2 SO 4 is 3 mol/L. The assembled vanadium redox flow battery has a current efficiency of 99%, a voltage efficiency of 83%, and an energy efficiency of 82%.
实施例4 Example 4
将实施例2中的含金刚烷结构聚芳醚酮阴离子交换膜组装全钒液流电池,石墨毡为电极,石墨板为双极板,膜有效面积为5cm2,电流密度为100 mA/cm2,电解液中钒离子浓度为1.5mol/L,H2SO4浓度为3 mol/L。组装的全钒液流电池的电流效率为99%,电压效率为80%,能量效率为79%。 An all-vanadium redox flow battery was assembled with the adamantane-containing polyaryletherketone anion exchange membrane in Example 2, the graphite felt was used as the electrode, the graphite plate was used as a bipolar plate, the effective area of the membrane was 5 cm 2 , and the current density was 100 mA/cm 2. The concentration of vanadium ions in the electrolyte is 1.5 mol/L, and the concentration of H 2 SO 4 is 3 mol/L. The assembled all-vanadium redox flow battery has a current efficiency of 99%, a voltage efficiency of 80%, and an energy efficiency of 79%.
比较例 comparative example
与实施例3和4相比,将膜换成杜邦公司生产的商业化Nafion117膜,其他测试条件相同。全钒液流电池的电流效率为96%,电压效率80%,能量效率为77%。 Compared with Examples 3 and 4, the membrane was replaced with a commercial Nafion117 membrane produced by DuPont, and other test conditions were the same. The current efficiency of the vanadium redox flow battery is 96%, the voltage efficiency is 80%, and the energy efficiency is 77%.
与商业化Nafion膜相比,制备的含金刚烷结构聚芳醚阴离子交换膜,有优良的阻钒性能,在电流效率和能量效率均优于Nafion膜,而且膜的制备成本远低于全氟磺酸型的Nafion膜,在全钒液流电池领域具有很好的应用前景。 Compared with commercial Nafion membranes, the prepared adamantane-containing polyarylether anion exchange membranes have excellent resistance to vanadium, and are superior to Nafion membranes in current efficiency and energy efficiency, and the preparation cost of the membranes is much lower than that of perfluorinated membranes. The sulfonic acid-type Nafion membrane has good application prospects in the field of all-vanadium redox flow batteries.
对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本发明精神或范围的情况下,在其他实施例中实现。因此,本发明将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。 The above description of the disclosed embodiments enables those skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
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| CN105921029A (en) * | 2016-05-12 | 2016-09-07 | 安徽国能亿盛环保科技有限公司 | Technology for preparing composite nanofiltration membrane for water treatment |
| CN106268375A (en) * | 2016-08-14 | 2017-01-04 | 太原市晋华恒远科技有限公司 | A kind of preparation method of ion liquid functionalization polyphenylene sulfide porous film |
| CN106268375B (en) * | 2016-08-14 | 2018-09-11 | 太原市晋华恒远科技有限公司 | A kind of preparation method of ion liquid functionalization polyphenylene sulfide porous film |
| CN106268381A (en) * | 2016-08-30 | 2017-01-04 | 合肥工业大学 | A kind of anion exchange membrane of resistance to alkaline hydrolysis material and its preparation method and application |
| CN106268381B (en) * | 2016-08-30 | 2019-02-12 | 合肥工业大学 | A kind of alkaline hydrolysis-resistant anion exchange membrane material and preparation method and application thereof |
| CN108232225A (en) * | 2018-01-02 | 2018-06-29 | 泰顺永庆电力技术有限公司 | A kind of diaphragm of vanadium cell containing adamantane structure and preparation method thereof |
| CN116688778A (en) * | 2023-04-20 | 2023-09-05 | 云南中烟再造烟叶有限责任公司 | Random polyarylether nitrile sulfone membrane containing adamantane and preparation method thereof |
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